US4714719A - Catalyst for preparation of polyurethane and process for the preparation - Google Patents
Catalyst for preparation of polyurethane and process for the preparation Download PDFInfo
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- US4714719A US4714719A US06/927,287 US92728786A US4714719A US 4714719 A US4714719 A US 4714719A US 92728786 A US92728786 A US 92728786A US 4714719 A US4714719 A US 4714719A
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G18/00—Polymeric products of isocyanates or isothiocyanates
- C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
- C08G18/08—Processes
- C08G18/16—Catalysts
- C08G18/18—Catalysts containing secondary or tertiary amines or salts thereof
- C08G18/1825—Catalysts containing secondary or tertiary amines or salts thereof having hydroxy or primary amino groups
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
- B01J3/02—Feed or outlet devices therefor
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S526/901—Monomer polymerized in vapor state in presence of transition metal containing catalyst
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S526/908—Containing catalyst of specified particle size
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S526/909—Polymerization characterized by particle size of product
Definitions
- the invention relates to a process for preparing a polyurethane and in particular a catalyst to use in the preparation of polyurethanes such as flexible, rigid and semi-rigid polyurethanes and elastomers thereof. More particularly, the invention relates to a new catalyst used in the preparation of polyurethanes, which has an ether bond and a primary amino group in the molecule and only an extremely weak smell and which does not migrate in the polyurethane resin.
- metal catalysts based on, for example, tin, iron, titanium or manganese, or amine catalysts have been used and it is known that tertiary amines are preferably used as the catalysts in the preparation of polyurethanes.
- amines such as N-methylmorpholine, N-ethylmorpholine, triethylenediamine (1,4-diazabicyclo[2.2.2]octane), N,N,N',N'-tetramethyl-1,6-hexanediamine, N,N,N',N',N"-pentamethyldiethylenetriamine, N,N-dimethylcyclohexylamine and N,N-dimethylethanolamine have been used in the preparation of polyurethane.
- N,N-dimethylbenzylamine has been known as a tertiary amine catalyst having an activity nearly equal to that of a morpholine catalyst, the operation is difficult when this compound is used, since it is insoluble in water.
- weak catalysts include N-methylmorpholine, N-ethylmorpholine and N,N-dimethylbenzylamine. These weak catalysts play a quite important role to control the polyurethane preparation process delicately.
- N-methylmorpholine and N-ethylmorpholine have an extremely strong irritating smell and, when they are used in the preparation of polyurethane, the obtained polyurethane also has an irritating smell because the boiling points of N-methylmorpholine and N-ethylmorpholine are low.
- the catalyst remaining in the obtained product migrates into a substance in contact with the polyurethane (for example, a PVC coating formed on the polyurethane) to cause yellowing and to damage the commercial value of the product.
- N,N-dimethylbenzylamine is defective in that it has a strong irritating smell and, when it is used in the preparation of polyurethane, the obtained polyurethane requires a long curing time in the molding step before it is released from a mold and, therefore, the productivity is reduced disadvantageously.
- the urethane catalyst is used in the form of an aqueous amine solution usually in the preparation of a polyurethane foam, it is difficult to use N,N-dimethylbenzylamine in the form of an aqueous amine solution and, therefore, the workability is reduced seriously, since it has only a low solubility in water.
- Catalysts for the preparation of polyurethane resins which do not migrate in the polyurethane resins include those of the following general formula: ##STR2## wherein R 1 represents an independent alkyl group having 1 to 6 carbon atoms or the two R 1 groups may form a 3- to 6-membered heterocyclic ring with the nitrogen atom and R 2 represents a divalent organic group having no active group reactive with an isocyanate other than the amino group,
- Compounds used as the catalyst in the preparation of polyurethanes in the examples given in said specification include dimethylaminopropylamine, diethylaminopropylamine and N-(2-aminoethyl)aziridine.
- the invention provides a catalyst for preparation of a polyurethane, which comprises a compound having the formula: ##STR3## in which n is an integer of 2 to 12, A is hydrogen or a group of --CH2CHRCH2NH2 and R is hydrogen or methyl, provided that n is 6 when A is hydrogen.
- the compound for the catalyst of the invention includes two embodiments. One embodiment has the formula in which A is said group. The other has the formula in which A is hydrogen.
- the invention provides a process for preparing a polyurethane from a polyol and a polyisocyanate in the presence of a catalyst comprising a compound having the formula: ##STR4## in which n is an integer of 2 to 12, A is hydrogen or a group of --CH2CHRCH2NH2 and R is hydrogen or methyl, provided that n is 6 when A is hydrogen.
- the present invention provides a catalyst for the preparation of polyurethanes which comprises a compound of the general formula: ##STR5## wherein n represents an integer of 2 to 12 and
- R represents a hydrogen atom or a methyl group.
- the new catalyst of the present invention for the preparation of polyurethanes can be prepared easily by reacting an N,N-dimethylaminoalkanol having 2 to 12 carbon atoms in the alkanol moiety with acrylonitrile or methacrylonitrile to form a compound of the general formula: ##STR6## wherein n and R are as defined above, and then converting the CN group into a CH 2 NH 2 group by catalytic hydrogenation.
- the new catalyst of the present invention is used in an amount in the range of preferably 0.01 to 10 parts (by weight; the same shall apply hereinafter), particularly 0.1 to 4 parts, for 100 parts of a polyol used in the preparation of the polyurethane. It is also possible, however, to use the catalyst in an amount beyond said range for the purpose of realizing an optimum condition for the preparation of polyurethane by controlling the amount of the catalyst.
- the novel catalyst of the present invention can be used in combination with a tertiary amine such as triethylenediamine or an organometallic compound such as an organotin compound used usually as a cocatalyst in the preparation of polyurethanes.
- the polyisocyanate usable as the starting material for the polyurethanes in the presence of the new catalyst of the present invention may be any of known polyisocyanates such as 2,4-tolylene, 2,6-tolylene, 4,4'-diphenylmethane, hexamethylene, isophorone, lysine, xylylene, cyclohexane, toluidine, p-phenylene, o-phenylene, m-phenylene, 1,5-naphthylene, 4,4'-biphenyl, 3,3'-dimethylbiphenyl 4,4'-, and 3,3'-dimethoxybiphenyl 4,4'-diisocyanates.
- the polyols usable in the preparation of the polyurethane in the presence of the new catalyst of the present invention include known polyester polyols and polyether polyols. Examples of them include polyester polyols prepared from an ordinary dibasic acid and a polyhydric alcohol; polyether polyols obtained by adding ethylene oxide or propylene oxide to a polyhydric alcohol such as glycol, glycerol, pentaerythritol, trimethylolpropane or sucrose; and amine polyols obtained by adding ethylene oxide or propylene oxide to a polyamine such as triethylenediamine, tolylenediamine, 1,6-hexanediamine, 1,3-propionediamine or isophoronediamine.
- polyester polyols prepared from an ordinary dibasic acid and a polyhydric alcohol polyether polyols obtained by adding ethylene oxide or propylene oxide to a polyhydric alcohol such as glycol, glycerol, pentaerythritol, trimethyl
- Organic polyol reactants usable in the preparation of the polyurethane foams include polymer polyols. They are prepared by polymerizing one or more ethylenically unsaturated monomers dissolved or dispersed in any of other polyols mentioned herein in the presence of a free radical catalyst.
- the ethylenically unsaturated monomers may be used either alone or in the form of a mixture of them and typical examples of them include ethylene, propylene, acrylonitrile, vinyl chloride, vinylidene chloride, styrene, ⁇ -methylstyrene, methyl methacrylate and butadiene.
- Such a composition can be prepared usually by polymerizing the monomer in the polyol as the base in the presence of a free radical initiator comprising a peroxide, persulfate, percarbonate, perborate or azo compound at a temperature in the range of about 40° to 150° C.
- a free radical initiator comprising a peroxide, persulfate, percarbonate, perborate or azo compound at a temperature in the range of about 40° to 150° C.
- additives may be used, if necessary.
- the additives include, for example, foaming agents such as CFCl 3 and CH 2 Cl 2 , surfactants such as organopolysiloxanes, and flame retardants such as alkyl halides and phosphorus halides.
- foaming agents such as CFCl 3 and CH 2 Cl 2
- surfactants such as organopolysiloxanes
- flame retardants such as alkyl halides and phosphorus halides.
- the varieties and amounts of these additives may be the same as those used usually.
- the present invention provides a catalyst for the preparation of polyurethanes which comprises a compound of the formula: ##STR7##
- the catalyst of the invention to use for preparation of a polyurethane is obtained, for example, by reacting hexanediol with dimethylamine. Alternatively it is prepared easily by reacting 1-chloro-6-hydroxyhexane with dimethylamine.
- the new catalyst of the present invention for the preparation of polyurethanes has an extremely weak smell supposedly because its molecular weight is larger and its boiling point is higher than those of known catalysts.
- the catalyst of the present invention having a (CH 3 ) 2 N-group in the molecule, an activity suitable as the catalyst for the preparation of polyurethanes and the number of nitrogen atoms per molecular weight larger than that of known catalysts, the operation of the preparation of polyurethane can be controlled easily.
- the primary amino or hydroxy group of the compound reacts with the isocyanato group in the starting material of the polyurethane and is incorporated in the polyurethane molecule before the completion of the polyurethane-forming reaction. Therefore, no migration of the catalyst on the surface of the product is observed after completion of the curing and, accordingly, troubles due to the migration (such as yellowing and insufficient adhesion) can be avoided.
- the catalyst of the invention reacts with an isocyanate group in the process for preparation of a polyurethane to be incorporated chemically with resulting polyurethane molecules before the completion of the reaction. As a result, the catalyst does not migrate onto the resin surface. Thus, this catalyst for the preparation of polyurethanes is a non-migrating catalyst.
- This catalyst has only an extremely weak smell. It has a catalytic activity higher than those of N-methylmorpholine, N-ethylmorpholine and N,N-dimethylbenzylamine and, therefore, it has an economical advantage in that the amount thereof may be reduced.
- Tertiary amine urethane catalysts have been used in the form of an aqueous amine solution in the conventional processes for the preparation of polyurethanes.
- the new catalyst of the present invention for the preparation of polyurethane is highly soluble in water and, therefore, causes no trouble in the conventional processes for the preparation of polyurethanes.
- the catalyst of the present invention for the preparation of polyurethanes has a quite low volatility and, therefore, only a weak smell, since it has a relatively high molecular weight and a high boiling point. With this catalyst, the working environment in the preparation of polyurethanes can be improved remarkably.
- a polyurethane foam was prepared from starting materials used in amounts shown in Table 1 by an ordinary process. More particularly, a polyol, water, surfactant, catalyst, foaming agent and polyisocyanate were mixed together by stirring and the mixture was poured into a paper cup kept at 20° C. to form a urethane foam. In this step, the paper cup was not covered.
- the cream time means a time from the initiation of the mixing and stirring of the starting materials to just before the initiation of the foaming.
- the gel time is a time required for the sufficient polymerization until stringiness of the polyurethane foam is observed when a sharp-edged substance is brought into contact with the surface of the polyurethane foam and then taken out.
- the tack-free time means a time required until the polyurethane foam no more adheres to a finger when the finger touches it.
- the rise time means a time required until the apparent maximum height of the polyurethane foam is obtained.
- a polyurethane foam was prepared from starting materials used in amounts shown in Table 10 by an ordinary process. More particularly, a polyol, water, catalyst and polyisocyanate were mixed together by stirring and the mixture was poured into a paper cup to form a urethane foam. In this step, the paper cup was not covered. The amount of the catalyst used was controlled so that the rise time would be 50 ⁇ 5 sec.
- the vinyl chloride sheet used was prepared by kneading the components shown in Table 11 and pressing the mixture to obtain a sheet.
- MN-700 a glycerol-based polyether polyol having a molecular weight of about 700; a product of Mitsui Toatsu Co., Ltd.
- the smell of the solution was examined by 50 selected smell panelists. The results are shown in Table 13. The degree of the smell was divided into the following groups:
- the amount of the catalyst added is usually less than 10% (preferably 3 to 5%). It is apparent from the above table that the new catalyst of the present invention for the preparation of polyurethane has such an extremely weak smell.
- a polyurethane foam was prepared from starting materials used in amounts shown in Table 14 by an ordinary process. More particularly, a polyol, water, surfactant, catalyst, foaming agent and polyisocyanate were mixed together by stirring and the mixture was poured in a paper cup kept at 20° C. to form a urethane foam. In this step, the paper cup was not covered.
- the properties of the catalyst of the present invention and ordinary catalysts for the preparation of the polyurethanes were examined and the results are shown in Tables 15 to 17.
- the cream time means a time from the initiation of the mixing and stirring of the starting materials to just before the initiation of the foaming.
- the gel time is a time required for the sufficient polymerization until stringiness of the polyurethane foam is observed when a sharp-edged substance is brought into contact with the surface of the polyurethane foam and then taken out.
- the tack-free time means a time required until the polyurethane foam no more adheres to a finger when the finger touches it.
- the rise time means a time required until the apparent maximum height of the polyurethane foam is obtained.
- MN-700 a glycerol-based polyetherpolyol having a molecular weight of about 700; a product of Mitsui Toatsu Co., Ltd.
- MN-700 a glycerol-based polyetherpolyol having a molecular weight of about 700; a product of Mitsui Toatsu Co., Ltd.
- the smell of the solution was examined by 50 selected smell panelists. The degree of the smell was divided into the following groups:
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Abstract
A polyurethane is prepared with use of a catalyst comprising a compound having the formula: <IMAGE> in which n is an integer of 2 to 12, A is a hydrogen or a group of -CH2CHRCH2NH2 and R is hdyrogen or methyl, provided that n is 6 when A is hydrogen. The compound scarcely smells and does not elute out of the polyurethane article. The process is easy to control.
Description
The invention relates to a process for preparing a polyurethane and in particular a catalyst to use in the preparation of polyurethanes such as flexible, rigid and semi-rigid polyurethanes and elastomers thereof. More particularly, the invention relates to a new catalyst used in the preparation of polyurethanes, which has an ether bond and a primary amino group in the molecule and only an extremely weak smell and which does not migrate in the polyurethane resin.
For the preparation of polyurethanes, metal catalysts based on, for example, tin, iron, titanium or manganese, or amine catalysts have been used and it is known that tertiary amines are preferably used as the catalysts in the preparation of polyurethanes. For example, amines such as N-methylmorpholine, N-ethylmorpholine, triethylenediamine (1,4-diazabicyclo[2.2.2]octane), N,N,N',N'-tetramethyl-1,6-hexanediamine, N,N,N',N',N"-pentamethyldiethylenetriamine, N,N-dimethylcyclohexylamine and N,N-dimethylethanolamine have been used in the preparation of polyurethane. Though N,N-dimethylbenzylamine has been known as a tertiary amine catalyst having an activity nearly equal to that of a morpholine catalyst, the operation is difficult when this compound is used, since it is insoluble in water.
Among these catalysts used in the preparation of polyurethanes, those having a relatively low activity (weak catalysts) include N-methylmorpholine, N-ethylmorpholine and N,N-dimethylbenzylamine. These weak catalysts play a quite important role to control the polyurethane preparation process delicately.
However, the weak catalysts for the preparation of polyurethanes heretofore proposed have many problems. That is, N-methylmorpholine and N-ethylmorpholine have an extremely strong irritating smell and, when they are used in the preparation of polyurethane, the obtained polyurethane also has an irritating smell because the boiling points of N-methylmorpholine and N-ethylmorpholine are low. When such a compound is used in the preparation of the polyurethane, the catalyst remaining in the obtained product migrates into a substance in contact with the polyurethane (for example, a PVC coating formed on the polyurethane) to cause yellowing and to damage the commercial value of the product. N,N-dimethylbenzylamine is defective in that it has a strong irritating smell and, when it is used in the preparation of polyurethane, the obtained polyurethane requires a long curing time in the molding step before it is released from a mold and, therefore, the productivity is reduced disadvantageously. Though the urethane catalyst is used in the form of an aqueous amine solution usually in the preparation of a polyurethane foam, it is difficult to use N,N-dimethylbenzylamine in the form of an aqueous amine solution and, therefore, the workability is reduced seriously, since it has only a low solubility in water.
Catalysts for the preparation of polyurethane resins which do not migrate in the polyurethane resins include those of the following general formula: ##STR2## wherein R1 represents an independent alkyl group having 1 to 6 carbon atoms or the two R1 groups may form a 3- to 6-membered heterocyclic ring with the nitrogen atom and R2 represents a divalent organic group having no active group reactive with an isocyanate other than the amino group,
as disclosed in the specification of Japanese Patent Laid-Open No. 4846/1971. Compounds used as the catalyst in the preparation of polyurethanes in the examples given in said specification include dimethylaminopropylamine, diethylaminopropylamine and N-(2-aminoethyl)aziridine.
However, these compounds have problems with respect to working atmosphere, since they have a low boiling point due to their small molecular weight and an extremely strong irritating smell.
The invention provides a catalyst for preparation of a polyurethane, which comprises a compound having the formula: ##STR3## in which n is an integer of 2 to 12, A is hydrogen or a group of --CH2CHRCH2NH2 and R is hydrogen or methyl, provided that n is 6 when A is hydrogen.
The compound for the catalyst of the invention includes two embodiments. One embodiment has the formula in which A is said group. The other has the formula in which A is hydrogen.
Further the invention provides a process for preparing a polyurethane from a polyol and a polyisocyanate in the presence of a catalyst comprising a compound having the formula: ##STR4## in which n is an integer of 2 to 12, A is hydrogen or a group of --CH2CHRCH2NH2 and R is hydrogen or methyl, provided that n is 6 when A is hydrogen.
The invention will be below explained in detail first in reference to the first embodiment of the catalyst compound. Then it will be disclosed also about the second embodiment.
After intensive investigations made for the purpose of solving the above-mentioned problems, the inventors have found that compounds having an ether bond and a primary amino group in the molecule have an extremely weak smell and an activity suitable as the catalyst for the preparation of polyurethanes and that, after the preparation of the polyurethane, these compounds do not migrate in said resin. The present invention has been completed on the basis of this finding.
The present invention provides a catalyst for the preparation of polyurethanes which comprises a compound of the general formula: ##STR5## wherein n represents an integer of 2 to 12 and
R represents a hydrogen atom or a methyl group.
The new catalyst of the present invention for the preparation of polyurethanes can be prepared easily by reacting an N,N-dimethylaminoalkanol having 2 to 12 carbon atoms in the alkanol moiety with acrylonitrile or methacrylonitrile to form a compound of the general formula: ##STR6## wherein n and R are as defined above, and then converting the CN group into a CH2 NH2 group by catalytic hydrogenation.
The new catalyst of the present invention is used in an amount in the range of preferably 0.01 to 10 parts (by weight; the same shall apply hereinafter), particularly 0.1 to 4 parts, for 100 parts of a polyol used in the preparation of the polyurethane. It is also possible, however, to use the catalyst in an amount beyond said range for the purpose of realizing an optimum condition for the preparation of polyurethane by controlling the amount of the catalyst. The novel catalyst of the present invention can be used in combination with a tertiary amine such as triethylenediamine or an organometallic compound such as an organotin compound used usually as a cocatalyst in the preparation of polyurethanes.
The polyisocyanate usable as the starting material for the polyurethanes in the presence of the new catalyst of the present invention may be any of known polyisocyanates such as 2,4-tolylene, 2,6-tolylene, 4,4'-diphenylmethane, hexamethylene, isophorone, lysine, xylylene, cyclohexane, toluidine, p-phenylene, o-phenylene, m-phenylene, 1,5-naphthylene, 4,4'-biphenyl, 3,3'-dimethylbiphenyl 4,4'-, and 3,3'-dimethoxybiphenyl 4,4'-diisocyanates.
The polyols usable in the preparation of the polyurethane in the presence of the new catalyst of the present invention include known polyester polyols and polyether polyols. Examples of them include polyester polyols prepared from an ordinary dibasic acid and a polyhydric alcohol; polyether polyols obtained by adding ethylene oxide or propylene oxide to a polyhydric alcohol such as glycol, glycerol, pentaerythritol, trimethylolpropane or sucrose; and amine polyols obtained by adding ethylene oxide or propylene oxide to a polyamine such as triethylenediamine, tolylenediamine, 1,6-hexanediamine, 1,3-propionediamine or isophoronediamine. Organic polyol reactants usable in the preparation of the polyurethane foams include polymer polyols. They are prepared by polymerizing one or more ethylenically unsaturated monomers dissolved or dispersed in any of other polyols mentioned herein in the presence of a free radical catalyst. The ethylenically unsaturated monomers may be used either alone or in the form of a mixture of them and typical examples of them include ethylene, propylene, acrylonitrile, vinyl chloride, vinylidene chloride, styrene, α-methylstyrene, methyl methacrylate and butadiene. Such a composition can be prepared usually by polymerizing the monomer in the polyol as the base in the presence of a free radical initiator comprising a peroxide, persulfate, percarbonate, perborate or azo compound at a temperature in the range of about 40° to 150° C.
In the preparation of the polyurethanes in the presence of the new catalyst of the present invention, additives may be used, if necessary. The additives include, for example, foaming agents such as CFCl3 and CH2 Cl2, surfactants such as organopolysiloxanes, and flame retardants such as alkyl halides and phosphorus halides. The varieties and amounts of these additives may be the same as those used usually.
The above relates to the first embodiment of the compound for the catalyst of the invention. Instead the second embodiment shown below may be used in the same way as shown above in the invention.
After intensive investigations made for the purpose of solving the above-mentioned problems, the inventors have found that compounds having dimethylamino and primary hydroxyl groups in the molecule have an extremely weak smell and properties suitable as the catalyst for the preparation of polyurethanes. The present invention has been completed on the basis of this finding.
The present invention provides a catalyst for the preparation of polyurethanes which comprises a compound of the formula: ##STR7##
The catalyst of the invention to use for preparation of a polyurethane is obtained, for example, by reacting hexanediol with dimethylamine. Alternatively it is prepared easily by reacting 1-chloro-6-hydroxyhexane with dimethylamine.
The new catalyst of the present invention for the preparation of polyurethanes has an extremely weak smell supposedly because its molecular weight is larger and its boiling point is higher than those of known catalysts. With the catalyst of the present invention having a (CH3)2 N-group in the molecule, an activity suitable as the catalyst for the preparation of polyurethanes and the number of nitrogen atoms per molecular weight larger than that of known catalysts, the operation of the preparation of polyurethane can be controlled easily. Further the primary amino or hydroxy group of the compound reacts with the isocyanato group in the starting material of the polyurethane and is incorporated in the polyurethane molecule before the completion of the polyurethane-forming reaction. Therefore, no migration of the catalyst on the surface of the product is observed after completion of the curing and, accordingly, troubles due to the migration (such as yellowing and insufficient adhesion) can be avoided.
The catalyst of the invention reacts with an isocyanate group in the process for preparation of a polyurethane to be incorporated chemically with resulting polyurethane molecules before the completion of the reaction. As a result, the catalyst does not migrate onto the resin surface. Thus, this catalyst for the preparation of polyurethanes is a non-migrating catalyst. This catalyst has only an extremely weak smell. It has a catalytic activity higher than those of N-methylmorpholine, N-ethylmorpholine and N,N-dimethylbenzylamine and, therefore, it has an economical advantage in that the amount thereof may be reduced. Tertiary amine urethane catalysts have been used in the form of an aqueous amine solution in the conventional processes for the preparation of polyurethanes. The new catalyst of the present invention for the preparation of polyurethane is highly soluble in water and, therefore, causes no trouble in the conventional processes for the preparation of polyurethanes.
Now, the detailed description will be made on the non-migrating property of the catalyst. When a monolithic molding is prepared from a polyurethane foam and a vinyl chloride sheet in the presence of, a known catalyst such as N,N-dimethylbenzylamine (DMBA), the amine migrates from the polyurethane foam into the vinyl chloride sheet after completion of the foaming and curing and the vinyl chloride sheet is yellowed gradually disadvantageously. This phenomenon is accelerated by heating or other means and this is a serious problem in the automobile industry wherein a lot of moldings of this type are used. However, when the catalyst of the present invention for the preparation of polyurethane is used, the catalyst does not migrate from the polyurethane foam so that said problems can be solved.
Further, the catalyst of the present invention for the preparation of polyurethanes has a quite low volatility and, therefore, only a weak smell, since it has a relatively high molecular weight and a high boiling point. With this catalyst, the working environment in the preparation of polyurethanes can be improved remarkably.
The following examples and comparative examples will further illustrate the present invention, which by no means limit the invention.
A polyurethane foam was prepared from starting materials used in amounts shown in Table 1 by an ordinary process. More particularly, a polyol, water, surfactant, catalyst, foaming agent and polyisocyanate were mixed together by stirring and the mixture was poured into a paper cup kept at 20° C. to form a urethane foam. In this step, the paper cup was not covered.
The results are shown in Tables 2 to 9. In the tables, the cream time means a time from the initiation of the mixing and stirring of the starting materials to just before the initiation of the foaming. The gel time is a time required for the sufficient polymerization until stringiness of the polyurethane foam is observed when a sharp-edged substance is brought into contact with the surface of the polyurethane foam and then taken out. The tack-free time means a time required until the polyurethane foam no more adheres to a finger when the finger touches it. The rise time means a time required until the apparent maximum height of the polyurethane foam is obtained.
TABLE 1
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Component Parts by weight
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454AR*.sup.1 70.0
SBU-0478*.sup.2 20.0
MN-700*.sup.3 10.0
Water 1.5
L-5340*.sup.4 1.5
Freon-11 40.0
Tertiary amine varied as shown
urethane catalyst
in Tables 2 to 9
Isocyanate TR-50BX*.sup.5
index 105
______________________________________
*.sup.1 An aromatic amine polyol (OHV:450) (a product of Asahi Olin)
*.sup.2 A sugar polyether polyol (OHV:530) (a product of Sumitomo Bayer
Urethane)
*.sup.3 A glycerol polyether polyol (OHV:235) (a product of Mitsui Toatsu
Urethane)
*.sup.4 A surfactant of Nippon Unicar
*.sup.5 An isocyanate of Mitsui Toatsu Urethane (a mixture of crude MDI
with TDI prepolymer; NCO: 31%).
TABLE 2
______________________________________
Cases in which N,N--dimethylaminohexyl
3-aminopropyl ether was used as the catalyst
(substantially no irritating smell recognized)
Amount (parts)
Example 1 2.0 4.0 6.0 8.0
______________________________________
Cream time (sec)
16 10 8 6
Gel time (sec) 120 71 50 33
Tack-free time (sec)
180 91 60 45
Rise time (sec)
204 122 88 65
______________________________________
TABLE 3
______________________________________
Cases in which N,N--dimethylaminoethyl
3-aminopropyl ether was used as the catalyst
(substantially no irritating smell recognized)
Amount (parts)
Example 2 2.0 4.0 6.0 8.0
______________________________________
Cream time (sec)
13 7 6 4
Gel time (sec) 119 72 52 32
Tack-free time (sec)
181 90 60 42
Rise time (sec)
200 123 85 66
______________________________________
TABLE 4
______________________________________
Cases in which N,N--dimethylaminohexyl
2-methyl-3-aminopropyl ether was used as the
catalyst (substantially no irritating smell recognized)
Amount (parts)
Example 3 2.0 4.0 6.0 8.0
______________________________________
Cream time (sec)
14 9 6 5
Gel time (sec) 115 64 42 32
Tack-free time (sec)
170 98 54 42
Rise time (sec)
194 114 84 60
______________________________________
TABLE 5
______________________________________
Cases in which N,N--dimethylaminoethyl
2-methyl-3-aminopropyl ether was used as the
catalyst (substantially no irritating smell recognized)
Amount (parts)
Example 4 2.0 4.0 6.0 8.0
______________________________________
Cream time (sec)
13 8 6 5
Gel time (sec) 118 69 44 36
Tack-free time (sec)
176 102 56 44
Rise time (sec)
199 120 88 62
______________________________________
TABLE 6
______________________________________
Cases in which N,N--dimethylbenzylamine was used
as the catalyst (a strong irritating smell recognized)
Comparative Amount (parts)
Example 1 7.5 10.0
______________________________________
Cream time (sec) 13 8
Gel time (sec) 91 80
Tack-free time (sec)
140 100
Rise time (sec) 160 130
______________________________________
When the values similar to those obtained by using the catalysts of the present invention are to be obtained by using N,N-dimethylbenzylamine, the amount of this catalyst must be increased to an economically disadvantageous amount.
TABLE 7
______________________________________
Cases in which N--methylmorpholine
N--ethylmorpholine was used as the catalyst
(a strong irritating smell recognized)
N--methyl-
N--ethyl-
Comparative morpholine
morpholine
Examples 2 and 3 10 parts 10 parts
______________________________________
Cream time (sec) 11 16
Gel time (sec) 100 150
Tack-free time (sec)
160 250
Rise time (sec) 160 230
______________________________________
When the values similar to those obtained by using the catalysts of the present invention are to be obtained by using N-methylmorpholine or N-ethylmorpholine, the amount of this catalyst must be increased to an economically disadvantageous amount.
TABLE 8
______________________________________
Cases in which dimethylaminopropylamine was used
as the catalyst (an irritating smell recognized)
Comparative Amount (parts)
Example 4 2.0 4.0
______________________________________
Cream time (sec) 15 9
Gel time (sec) 59 34
Tack-free time (sec)
99 52
Rise time (sec) 135 80
______________________________________
It is known that when the human body is stained with dimethylaminopropylamine, it is poisoned with this compound to cause a rash or the like.
TABLE 9
______________________________________
Cases in which N--(2-aminoethyl)aziridine was used
as the catalyst (an irritating smell recognized)
Comparative Amount (parts)
Example 5 2.0 4.0
______________________________________
Cream time (sec) 9 5
Gel time (sec) 73 44
Tack-free time (sec)
115 63
Rise time (sec) 195 121
______________________________________
A polyurethane foam was prepared from starting materials used in amounts shown in Table 10 by an ordinary process. More particularly, a polyol, water, catalyst and polyisocyanate were mixed together by stirring and the mixture was poured into a paper cup to form a urethane foam. In this step, the paper cup was not covered. The amount of the catalyst used was controlled so that the rise time would be 50±5 sec.
The vinyl chloride sheet used was prepared by kneading the components shown in Table 11 and pressing the mixture to obtain a sheet.
Samples weighing about 3 g were cut out of the obtained polyurethane foam, placed in an about 130-cm3 sample bottle together with a vinyl chloride sheet having an area of 16 cm2 and left to stand in a constant temperature bath at 110° C. for 24 h. After cooling to room temperature, the degree of yellowing of the vinyl chloride sheet was determined by measuring the yellow index. The results are shown in Table 12.
TABLE 10
______________________________________
Component Parts by weight
______________________________________
Excenol-840*.sup.1
100
E-17*.sup.2 8.0
MN-300*.sup.3 8.0
Water 2.2
SBU 44 V 20*.sup.4
Index 105
Catalyst for the*.sup.5
preparation of
polyurethane
______________________________________
*.sup.1 A glycerol polyether polyol (molecular weight: about 6500, OHV:
26) (a product of Asahi Olin)
*.sup.2 A dimer acid polyester (OHV: 360) (a product of Kao Co., Ltd.)
*.sup.3 A polyether polyol (a product of Mitsui Toatsu Urethane)
*.sup.4 Crude MDI (a product of Sumitomo Bayer Urethane)
*.sup.5 Controlled so that the rise time would be 50 ± 5 sec.
TABLE 11
______________________________________
Component Parts by weight
______________________________________
Polyvinyl chloride
100
Dioctyl phthalate 50
Stabilizer 2.5
Heavy calcium carbonate
10
______________________________________
TABLE 12
______________________________________
Y.I.
______________________________________
Catalyst of Example 1 53.1
Catalyst of Example 2 54.7
Catalyst of Example 3 52.9
Catalyst of Example 4 54.8
Catalyst of Comparative Example 1
The sample
sheet was
blackened.
Catalyst of Comparative Example 2
135.1
Catalyst of Comparative Example 3
162.1
Catalyst of Comparative Example 4
90.1
Catalyst of Comparative Example 5
92.3
______________________________________
The smells of the catalysts of the present invention and the comparative catalysts were examined. Test method for checking the amine catalysts for the smell:
An amine urethane catalyst was dissolved in MN-700 (a glycerol-based polyether polyol having a molecular weight of about 700; a product of Mitsui Toatsu Co., Ltd.) to obtain a solution of a given concentration. The smell of the solution was examined by 50 selected smell panelists. The results are shown in Table 13. The degree of the smell was divided into the following groups:
⊚ : substantially no smell
○: faint smell
Δ: smell
X: strong smell
TABLE 13
______________________________________
Amine catalyst (%)
10 5 1 0.5 0.1
______________________________________
Product of the
present invention
N,N--Dimethylaminohexyl
○
○
○˜⊚
⊚
⊚
3-aminopropyl ether
N,N--Dimethylaminoethyl
○
○
○
⊚
⊚
3-aminopropyl ether
N,N--Dimethylaminohexyl
○
○
⊚
⊚
⊚
2-methyl-3-aminopropyl
ether
N,N--Dimethylaminoethyl
○
○
○˜⊚
⊚
⊚
2-methyl-3-aminopropyl
ether
Comparative product
N,N--Dimethylbenzylamine
X X X˜Δ
Δ
○
N--Methylmorpholine
X X X Δ
Δ
N--Ethylmorpholine
X X X˜Δ
Δ
Δ
Dimethylaminopropylamine
X X Δ
Δ
○
Dimethylaminoethylamine
X X X˜Δ
Δ
○
N--(2-Aminoethyl)aziridine
X X Δ
Δ
○
______________________________________
The amount of the catalyst added is usually less than 10% (preferably 3 to 5%). It is apparent from the above table that the new catalyst of the present invention for the preparation of polyurethane has such an extremely weak smell.
A polyurethane foam was prepared from starting materials used in amounts shown in Table 14 by an ordinary process. More particularly, a polyol, water, surfactant, catalyst, foaming agent and polyisocyanate were mixed together by stirring and the mixture was poured in a paper cup kept at 20° C. to form a urethane foam. In this step, the paper cup was not covered.
The properties of the catalyst of the present invention and ordinary catalysts for the preparation of the polyurethanes were examined and the results are shown in Tables 15 to 17. In the tables the cream time means a time from the initiation of the mixing and stirring of the starting materials to just before the initiation of the foaming. The gel time is a time required for the sufficient polymerization until stringiness of the polyurethane foam is observed when a sharp-edged substance is brought into contact with the surface of the polyurethane foam and then taken out. The tack-free time means a time required until the polyurethane foam no more adheres to a finger when the finger touches it. The rise time means a time required until the apparent maximum height of the polyurethane foam is obtained.
TABLE 14
______________________________________
Component Parts by weight
______________________________________
454AR*.sup.1 70.0
SBU-0478*.sup.2 20.0
MN-700*.sup.3 10.0
Water 1.5
L-5340*.sup.4 1.5
Freon-11 40.0
Tertiary amine varied as shown
urethane catalyst
in Tables 15 to 17
Isocyanate TR-50BX*.sup.5
index 105
______________________________________
*.sup.1 An aromatic amine polyol (OHV:450) (a product of Asahi Olin)
*.sup.2 A sugar polyether polyol (OHV:530) (a product of Sumitomo Bayer
Urethane)
*.sup.3 A glycerol polyether polyol (OHV:235) (a product of Mitsui Toatsu
Urethane)
*.sup.4 A surfactant of Nippon Unicar
*.sup.5 An isocyanate of Mitsui Toatsu Urethane (a mixture of crude MDI
with TDI prepolymer; NCO: 31%).?
TABLE 15
______________________________________
Cases in which the catalyst of the present invention
for the preparation of polyurethane was used
(no irritating smell recognized)
Amount (parts)
Example 7 2.0 3.0 4.0 5.0
______________________________________
Cream time (sec)
13 10 8 7
Gel time (sec) 95 73 57 43
Tack-free time (sec)
117 95 71 58
Rise time (sec)
163 124 104 80
______________________________________
TABLE 16
______________________________________
Cases in which dimethylaminoethanol was used as the
catalyst (an extremely strong bad recognized)
Comparative Amount (parts)
Example 7 2.0 3.0 4.0 5.0
______________________________________
Cream time (sec)
10 7 5 4
Gel time (sec) 110 83 61 50
Tack-free time (sec)
160 114 77 63
Rise time (sec)
195 148 120 93
______________________________________
TABLE 17
______________________________________
##STR8##
Amount (parts)
Comparative Example 8
2.0 4.0 6.0 8.0
______________________________________
Cream time (sec) 12 8 7 5
Gel time (sec) 150 100 75 57
Tack-free time (sec)
250 140 95 72
Rise time (sec) 280 170 133 107
______________________________________
The gelation caused when the catalyst for the preparation of polyurethane was mixed with water in the presence of a silicone surfactant was examined by the following method to obtain the results shown in Table 18.
62 g of water, 56 g of a silicone surfactant and 16 g of a catalyst were stirred together by means of a miniature motor and the gelation of the mixture was examined.
TABLE 18
______________________________________
Gelation
______________________________________
Catalyst of the present invention
not gelled
Comparative catalyst
Dimethylethanolamine gelled
##STR9## gelled
##STR10## gelled
______________________________________
The smells of the catalysts of the present invention and the comparative catalysts for the preparation of polyurethanes were examined. The results are shown in Table 19.
An amine urethane catalyst was dissolved in MN-700 (a glycerol-based polyetherpolyol having a molecular weight of about 700; a product of Mitsui Toatsu Co., Ltd.) to obtain a solution of a given concentration. The smell of the solution was examined by 50 selected smell panelists. The degree of the smell was divided into the following groups:
⊚ : substantially no smell
○: faint smell
Δ: smell
x: strong smell
TABLE 19
______________________________________
Amine catalyst (%)
10 5 1 0.5 0.1
______________________________________
Dimethylaminohexanol
○
○
⊚
⊚
⊚
N,N--Dimethylbenzylamine
X X X˜Δ
Δ
○
N--Methylmorpholine
X X X Δ
Δ
N--Ethylmorpholine
X X X˜Δ
Δ
Δ
Dimethylaminoethanol
X X Δ
Δ
Δ
______________________________________
Claims (7)
1. A process for preparing a polyurethane which comprises reacting a polyol and a polyisocyanate in the presence of a catalyst comprising a compound having the formula: ##STR11## in which n is an integer of 2 to 12, A is CH2 CHRCH2 NH2 and R is hydrogen or methyl.
2. A process as claimed in claim 1, in which 0.01 to 10 parts by weight of said compound is used per 100 parts by weight of the polyol.
3. A process as claimed in claim 1, in which the reaction is effected further in the presence of a tertiary amine polyurethane-forming co-catalyst and/or an organic tin compound polyurethane forming co-catalyst.
4. A process as claimed in claim 1, in which n is 2.
5. A process as claimed in claim 1, in which n is 6.
6. A process as claimed in claim 4, in which R is methyl.
7. A process as claimed in claim 5, in which R is methyl.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60-254085 | 1985-11-13 | ||
| JP60254085A JPS62115015A (en) | 1985-11-13 | 1985-11-13 | Catalyst for production of polyurethane |
| JP60254087A JPS62115017A (en) | 1985-11-13 | 1985-11-13 | Catalyst for production of polyurethane |
| JP60-254087 | 1985-11-13 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4714719A true US4714719A (en) | 1987-12-22 |
Family
ID=26541525
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US06/927,287 Expired - Fee Related US4714719A (en) | 1985-11-13 | 1986-11-04 | Catalyst for preparation of polyurethane and process for the preparation |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US4714719A (en) |
| KR (1) | KR910004075B1 (en) |
| CN (2) | CN1007255B (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4789689A (en) * | 1987-10-29 | 1988-12-06 | Texaco Inc. | Amine catalyst for urethanes |
| GB2231878A (en) * | 1989-05-22 | 1990-11-28 | Basf Corp | Molded flexible polyurethane compositions of polycarbonate compatibility |
| WO2001044337A1 (en) * | 1999-12-17 | 2001-06-21 | Kao Corporation | Process for producing polyurethane |
| US6306918B1 (en) | 1999-03-09 | 2001-10-23 | Kao Corporation | Semi-rigid polyurethane foam |
| US6410608B1 (en) | 1998-07-31 | 2002-06-25 | Kao Corporation | Process for producing polyurethane foam |
| KR100676118B1 (en) * | 1999-03-09 | 2007-02-01 | 카오카부시키가이샤 | Semi-rigid polyurethane foam |
| KR100695197B1 (en) | 2005-03-18 | 2007-03-19 | 에어 프로덕츠 앤드 케미칼스, 인코오포레이티드 | Foaming catalyst composition containing hydroxyl and surface active groups for the production of polyurethane foam |
| EP2162480A1 (en) * | 2007-06-19 | 2010-03-17 | Huntsman Petrochemical LLC | Reactive amine catalysts for polyurethane foam |
| WO2013182345A1 (en) * | 2012-06-06 | 2013-12-12 | Huntsman Petrochemical Llc | Amine suitable as pu-catalyst |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6849362B2 (en) * | 2016-09-28 | 2021-03-24 | 旭化成株式会社 | Polycarbonate diol composition |
| CN110248976A (en) * | 2016-12-02 | 2019-09-17 | 罗地亚经营管理公司 | The method for being used to prepare polyurethane foam |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4438235A (en) * | 1982-09-30 | 1984-03-20 | Basf Wyandotte Corporation | Tertiary alkanolamines to increase viscosity of filled liquid polymers |
-
1986
- 1986-11-04 US US06/927,287 patent/US4714719A/en not_active Expired - Fee Related
- 1986-11-12 KR KR1019860009553A patent/KR910004075B1/en not_active IP Right Cessation
- 1986-11-13 CN CN86107796A patent/CN1007255B/en not_active Expired
-
1989
- 1989-11-03 CN CN86108794A patent/CN1010783B/en not_active Expired
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4438235A (en) * | 1982-09-30 | 1984-03-20 | Basf Wyandotte Corporation | Tertiary alkanolamines to increase viscosity of filled liquid polymers |
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4789689A (en) * | 1987-10-29 | 1988-12-06 | Texaco Inc. | Amine catalyst for urethanes |
| GB2231878A (en) * | 1989-05-22 | 1990-11-28 | Basf Corp | Molded flexible polyurethane compositions of polycarbonate compatibility |
| US4980385A (en) * | 1989-05-22 | 1990-12-25 | Basf Corporation | Polyurethane/polycarbonate compatibility |
| US6410608B1 (en) | 1998-07-31 | 2002-06-25 | Kao Corporation | Process for producing polyurethane foam |
| KR100676118B1 (en) * | 1999-03-09 | 2007-02-01 | 카오카부시키가이샤 | Semi-rigid polyurethane foam |
| US6306918B1 (en) | 1999-03-09 | 2001-10-23 | Kao Corporation | Semi-rigid polyurethane foam |
| US20030004220A1 (en) * | 1999-12-17 | 2003-01-02 | Atsushi Ishikawa | Process for producing polyurethane |
| US6767929B2 (en) | 1999-12-17 | 2004-07-27 | Kao Corporation | Process for producing polyurethane |
| WO2001044337A1 (en) * | 1999-12-17 | 2001-06-21 | Kao Corporation | Process for producing polyurethane |
| KR100695197B1 (en) | 2005-03-18 | 2007-03-19 | 에어 프로덕츠 앤드 케미칼스, 인코오포레이티드 | Foaming catalyst composition containing hydroxyl and surface active groups for the production of polyurethane foam |
| EP2162480A1 (en) * | 2007-06-19 | 2010-03-17 | Huntsman Petrochemical LLC | Reactive amine catalysts for polyurethane foam |
| EP2162480A4 (en) * | 2007-06-19 | 2014-01-22 | Huntsman Petrochemical Llc | Reactive amine catalysts for polyurethane foam |
| WO2013182345A1 (en) * | 2012-06-06 | 2013-12-12 | Huntsman Petrochemical Llc | Amine suitable as pu-catalyst |
| CN104661993A (en) * | 2012-06-06 | 2015-05-27 | 亨茨曼石化产品有限责任公司 | Amine suitable as pu-catalyst |
| US9505870B2 (en) | 2012-06-06 | 2016-11-29 | Huntsman Petrochemical Llc | Amine suitable as PU-catalyst |
| CN104661993B (en) * | 2012-06-06 | 2017-07-21 | 亨茨曼石化产品有限责任公司 | It is suitable as the amine of catalysts for polyurethanes |
| EP2676949A1 (en) * | 2012-06-19 | 2013-12-25 | Huntsman Petrochemical LLC | Amine suitable as PU-catalyst |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1010783B (en) | 1990-12-12 |
| KR870004732A (en) | 1987-06-01 |
| CN1042922A (en) | 1990-06-13 |
| CN86107796A (en) | 1987-05-20 |
| CN1007255B (en) | 1990-03-21 |
| KR910004075B1 (en) | 1991-06-22 |
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